Comparison study on the adsorption of CFC - 115 and HFC - 125 on activated carbon and silicalite - 1 / Yong Peng in Industrial & engineering chemistry research, Vol. 49 N° 20 (Octobre 2010)  

Public ISBD [article]  inIndustrial & engineering chemistry research > Vol. 49 N° 20 (Octobre 2010) . - pp. 10009–10015 Titre : Comparison study on the adsorption of CFC - 115 and HFC - 125 on activated carbon and silicalite - 1 Type de document : texte imprimé Auteurs : Yong Peng, Auteur ; Fumin Zhang, Auteur ; Xiao Zheng, Auteur Année de publication : 2011 Article en page(s) : pp. 10009–10015 Note générale : Chimie industrielle Langues : Anglais (eng) Mots-clés : Adsorption Activated carbon Silicalite Résumé : The adsorption isotherms of CFC-115 (1-chloro-1,1,2,2,2-pentafluoroethane) and HFC-125 (1,1,1,2,2-pentafluoroethane) on Vruf activated carbon (Calgon Carbon Corp.; brand code, VRU-F) and silicalite-1 have been accurately measured at pressures up to 120 kPa and temperatures ranging from 273 to 348 K. The Tóth or dual-site Langmuir (DSL) model appropriately describes the equilibrium data for the adsorptives CFC-115 and HFC-125 on Vruf carbon or silicalite-1, respectively. Because HFC-125 molecule has a higher packing efficiency in the pores of Vruf carbon, its saturation capacity extracted by the Tóth model is higher than that for CFC-115. For CFC-115, a “kink” in the isotherm on silicalite-1 is observed at about 4 molecules (unit cell of silicalite-1)−1, and the measured isotherms of CFC-115 for the first time show a second-step adsorption at loadings over 4 molecules (unit cell)−1. This is ascribed to a large difference in the adsorption entropy between the molecular locations in the intersections and in the channels. The DSL model with fixed saturation capacities describes this behavior well. The mixture adsorption isotherms predicted by the ideal adsorbed solution theory show that both adsorbents could be industrially applicable in the separation of CFC-115 and HFC-125. DEWEY : 660 ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie1010806 [article] Comparison study on the adsorption of CFC - 115 and HFC - 125 on activated carbon and silicalite - 1 [texte imprimé] / Yong Peng, Auteur ; Fumin Zhang, Auteur ; Xiao Zheng, Auteur . - 2011 . - pp. 10009–10015. Chimie industrielle Langues : Anglais (eng) in Industrial & engineering chemistry research > Vol. 49 N° 20 (Octobre 2010) . - pp. 10009–10015 Mots-clés : Adsorption Activated carbon Silicalite Résumé : The adsorption isotherms of CFC-115 (1-chloro-1,1,2,2,2-pentafluoroethane) and HFC-125 (1,1,1,2,2-pentafluoroethane) on Vruf activated carbon (Calgon Carbon Corp.; brand code, VRU-F) and silicalite-1 have been accurately measured at pressures up to 120 kPa and temperatures ranging from 273 to 348 K. The Tóth or dual-site Langmuir (DSL) model appropriately describes the equilibrium data for the adsorptives CFC-115 and HFC-125 on Vruf carbon or silicalite-1, respectively. Because HFC-125 molecule has a higher packing efficiency in the pores of Vruf carbon, its saturation capacity extracted by the Tóth model is higher than that for CFC-115. For CFC-115, a “kink” in the isotherm on silicalite-1 is observed at about 4 molecules (unit cell of silicalite-1)−1, and the measured isotherms of CFC-115 for the first time show a second-step adsorption at loadings over 4 molecules (unit cell)−1. This is ascribed to a large difference in the adsorption entropy between the molecular locations in the intersections and in the channels. The DSL model with fixed saturation capacities describes this behavior well. The mixture adsorption isotherms predicted by the ideal adsorbed solution theory show that both adsorbents could be industrially applicable in the separation of CFC-115 and HFC-125. DEWEY : 660 ISSN : 0888-5885 En ligne : http://pubs.acs.org/doi/abs/10.1021/ie1010806

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